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Process Equipment and Plant Design

Process Equipment and Plant Design
Pressure drop (Δp) and the superficial gas mass velocity (G) in case of packed absorption tower operating in the preloading range are related as

Δp = 1/G0.6
Δp = G0.5
Δp = G2
Δp = G

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Process Equipment and Plant Design
Bracket supports are the most suitable for supporting __________ vessels.

Thin shperical (e.g. Horton sphere)
Thick walled vertical
Horizontal
None of these

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Process Equipment and Plant Design
Power required for agitation depends upon the

Height & properties of the liquid
Size of agitator & the tank
All of these
Agitator type & speed of agitation

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Process Equipment and Plant Design
The slope of operating line in the rectifying section of a distillation column is unity, if the reflux ratio is

∞
Minimum
0
1

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Process Equipment and Plant Design
An underdesigned steam trap will

Destroy itself of acceleration wear due to rapid recycling
Waste steam
Back up condensate and cause water hammer in steam line
None of these

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Process Equipment and Plant Design
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

0.55
0.8
0.99
0.95

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